Skip to main content

Advertisement

Log in

CFD analysis of a rotary kiln using for plaster production and discussion of the effects of flue gas recirculation application

  • Original
  • Published:
Heat and Mass Transfer Aims and scope Submit manuscript

Abstract

In this study, the CFD analysis of the rotary kiln is carried out for examining effects of various parameters on energy consumption and efficiency of the rotary kiln. The flue gas recirculation using in many applications is a useful method for combusting of fuel unburned in the flue gas. Also, effects of flue gas recirculation on the combusting of fuel, operating temperature and efficiency of the rotary kiln are discussed in this study. The rotary kiln, which is considered in this study, is used in plaster plant. Two different CFD models were created and these models are compared according to many parameters such as temperature distribution, mixture fraction, the mass fraction of O2, CO, CO and CH4 in the combustion chamber. It is found that the plaster plant has a great potential for an increase in energy efficiency. Results obtained for producers of rotary kiln and burner will be useful for determining better design parameters.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Institutional subscriptions

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8
Fig. 9
Fig. 10
Fig. 11
Fig. 12
Fig. 13
Fig. 14
Fig. 15
Fig. 16
Fig. 17
Fig. 18

Similar content being viewed by others

Abbreviations

C :

Constant

Cp :

Specific heat capacity (kJ/kg∙K)

\( \overrightarrow{F} \) :

Other forces (N)

G u :

Turbulence kinetic energy production rate (velocity)

G b :

Turbulence kinetic energy production rate (buoyancy)

\( \overrightarrow{g} \) :

Gravity (m/s2)

h :

Enthalpy (kJ/kg)

I :

Unit tensor.

i :

i-th content.

P :

Constant pressure (Pa)

Sh :

Radiative heat transfer and combustion rates

u :

Velocity (m/s)

:

Gradient operator

\( \overline{\overline{\tau}} \) :

Stress tensor

ρ :

Density (kg/m3)

Γ:

Diffusion coefficient (m2 / s)

ε :

Rate constant of turbulence kinetic energy (m2/s3)

α :

Turbulence model constant

μ :

Dynamic viscosity (Pa∙s)

References

  1. Marias F, Roustan H, Pichat A (2005) Modelling of a rotary kiln for the pyrolysis of aluminum waste. Chem Eng Sci 60:4609–4622. https://doi.org/10.1016/j.ces.2005.03.025

    Article  Google Scholar 

  2. Zhou B, Yang Y, Reuter MA, Boin UMJ (2005) CFD based process modeling of a rotary furnace for aluminum scrap melting. In: Fourth International Conference on CFD in the Oil and Gas, Metallurgical & Process Industries. Trondheim, pp 1–8

  3. Wang S, Lu J, Li W, et al (2006) Modeling of pulverized coal combustion in cement rotary kiln (PDF Download Available).pdf. 55:2350–2356

  4. Mujumdar KS, Ranade VV (2008) CFD modeling of rotary cement kilns. 2011 Int Symp Adv Control Ind Process 3:106–118. https://doi.org/10.1002/apj.123

    Google Scholar 

  5. Georgallis M, Nowak P, Salcudean M, Gartshore IS (2002) Mathematical modeling of lime kilns. Pulp Pap Canada 103:44–47

    Google Scholar 

  6. Zhang Z, Wang T (2009) Simulation of combustion and thermal-flow inside a petroleum coke rotary calcining kiln, part 1: process review and modeling. In: 2009 ASME International Mechanical Engineering Congress and Exposition. Florida, pp 1–11

  7. Hatzilyberis KS (2011) Design of an indirect heat rotary kiln gasifier. Fuel Process Technol 92:2429–2454. https://doi.org/10.1016/j.fuproc.2011.08.004

    Article  Google Scholar 

  8. Bhad TP, Sarkar S, Kaushik A, Herwadkar SV (2009) CFD modeling of a cement kiln with multi-channel burner for optimization of the flame profile. Seventh Int Conf CFD Miner Process Ind 1–7

  9. Granström BR, Lundström TS, Marjavaara BD, et al (2009) CFD modeling of the flow through a grate-kiln. In: Seventh International Conference on CFD in the Minerals and Process Industries. pp 1–6

  10. Cavazzuti M, Corticelli MA, Masina G, Saponelli R (2013) CFD analyses of syngas-fired industrial tiles kiln module. Eng Appl Comput Fluid Mech 7:533–543. https://doi.org/10.1080/19942060.2013.11015491

    Google Scholar 

  11. Aichun M, Jiemin Z (2002) CFD prediction of cold airflow field for multi-air channel pulverized coal burner in a rotary kiln. In: 37th Intersociety Energy Conversion Engineering Conference (IECEC). pp 418–421

  12. Macphee J, Sellier M, Jermy M, Tadulan E (2009) CFD modeling of pulverized coal combustion in a rotary lime kiln. Seventh Int Conf CFD Miner Process Ind 1–6

  13. Manju MS, Savithri S (2012) Three dimensional CFD simulation of pneumatic coal injection in a direct reduction rotary kiln. Fuel 102:54–64. https://doi.org/10.1016/j.fuel.2012.06.024

    Article  Google Scholar 

  14. Khaldi N, Chouari Y, Mhiri H, Bournot P (2016) CFD investigation on the flow and combustion in a 300 MWe tangentially fired pulverized-coal furnace. Heat Mass Transf und Stoffuebertragung 52:1881–1890. https://doi.org/10.1007/s00231-015-1710-4

    Article  Google Scholar 

  15. Elattar HF, Specht E, Fouda A, Bin-Mahfouz AS (2016) CFD modeling using PDF approach for investigating the flame length in rotary kilns. Heat Mass Transf und Stoffuebertragung 52:2635–2648. https://doi.org/10.1007/s00231-016-1768-7

    Article  Google Scholar 

  16. Kumar J, Bansal A (2012) CFD modeling of hydrodynamics and mass transfer of Rhodamine B in annular reactor. Heat Mass Transf und Stoffuebertragung 48:2069–2077. https://doi.org/10.1007/s00231-012-1052-4

    Article  Google Scholar 

  17. Guo Y, Deng B, Ge D, Shen X (2015) CFD simulation on hydrodynamics in fluidized beds: assessment of gradient approximations and turbulence models. Heat Mass Transfund Stoffuebertragung 51:1067–1074. https://doi.org/10.1007/s00231-014-1478-y

    Article  Google Scholar 

  18. Chernetskiy MY, Dekterev AA, Burdukov AP, Hanjalić K (2014) Computational modeling of autothermal combustion of mechanically-activated micronized coal. Fuel 135:443–458. https://doi.org/10.1016/j.fuel.2014.06.052

    Article  Google Scholar 

  19. Marias F (2003) A model of a rotary kiln incinerator including processes occurring within the solid and the gaseous phases. Comput Chem Eng 27:813–825. https://doi.org/10.1016/S0098-1354(02)00268-5

    Article  Google Scholar 

  20. Sofialidis D, Faltsi O, Sardi K et al (2005) Modelling low-temperature carbonization of solid fuels in a heated rotary kiln for clean fuel production. Fuel 84:2211–2221. https://doi.org/10.1016/j.fuel.2005.04.021

    Article  Google Scholar 

  21. Boateng AA (2008) Rotary kilns transport phenomena and transport processes. Elsevier Inc.

  22. Burstr P, Burstr P, Ljung A, et al (2013) Heat transfer through a randomly packed bed of spheres. 54:4–5

  23. Kriaa W, Bejaoui S, Mhiri H et al (2014) Study of dynamic structure and heat and mass transfer of a vertical ceramic tiles dryer using CFD simulations. Heat Mass Transf 50:235–251. https://doi.org/10.1007/s00231-013-1244-6

    Article  Google Scholar 

  24. Yang Y, Reuter MA, Hartman DTM (2003) CFD modelling for control of hazardous waste incinerator. Control Eng Pract 11:93–101. https://doi.org/10.1016/S0967-0661(02)00149-1

    Article  Google Scholar 

  25. Gürtürk M, Oztop HF (2014) Energy and exergy analysis of a rotary kiln used for plaster production. Appl Therm Eng 67:554–565. https://doi.org/10.1016/j.applthermaleng.2014.03.025

    Article  Google Scholar 

  26. Gürtürk M, Oztop HF (2016) Exergoeconomic analysis of a rotary kiln used for plaster production as building materials. Appl Therm Eng 104:486–496. https://doi.org/10.1016/j.applthermaleng.2016.05.106

    Article  Google Scholar 

  27. ANSYS (2015) Fluent theory guide. Knowl Creat Diffus Util 15317:724–746

  28. Docquier N, Candel S (2002) Combustion control and sensors: A review. Prog Energy Combust Sci 28:107–150. https://doi.org/10.1016/S0360-1285(01)00009-0

    Article  Google Scholar 

  29. Kuo KK (2005) Principles of combustion. John Wiley & Sons, New York

    Google Scholar 

  30. Mastorakos E, Massias A, Tsakiroglou CD et al (1999) CFD predictions for cement kilns including flame modelling, heat transfer and clinker chemistry. Appl Math Model 23:55–76. https://doi.org/10.1016/S0307-904X(98)10053-7

    Article  MATH  Google Scholar 

  31. ANSYS (2011) ANSYS Meshing User ’ s Guide. Knowl Creat Diffus Util 15317:724–746

    Google Scholar 

  32. Gürtürk M (2015) Performance Evaluation of a Plaster Production Plant Using Energy Exergy and Exergoeconomics Analyses. Fırat University

  33. Achim D, Naser J, Morsi YS, Pascoe S (2009) Numerical investigation of full scale coal combustion model of tangentially fired boiler with the effect of mill ducting. Heat Mass Transf und Stoffuebertragung 46:1–13. https://doi.org/10.1007/s00231-009-0539-0

    Article  Google Scholar 

  34. Mujumdar K, Ranade V (2006) Simulation of rotary cement kilns using a one-dimensional model. Chem Eng Res Des 84:165–177. https://doi.org/10.1205/cherd.04193

    Article  Google Scholar 

Download references

Acknowledgments

This work was supported by the Fırat University Project Support Unit under Grant (TEKF.13.01). Also, the authors are supported by Ar-alçı Company and would like to thank both FUBAP and Ar-alçı Company for their valuable contribution and support to this work.

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Mert Gürtürk.

Additional information

Publisher’s Note

Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Gürtürk, M., Oztop, H.F. & Pambudi, N.A. CFD analysis of a rotary kiln using for plaster production and discussion of the effects of flue gas recirculation application. Heat Mass Transfer 54, 2935–2950 (2018). https://doi.org/10.1007/s00231-018-2336-0

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s00231-018-2336-0

Navigation